Search
Post Requirements
Post Requirements
Product information
Anthraquinone dye rotary flash dryer
working principle
At the bottom of the anthraquinone dye rotary flash dryer, the larger and wet particle clusters are mechanically broken up under the action of the agitator, and the particles with lower moisture content and smaller particle size are entrained and lifted by the rotating airflow and further dried during the rise. Because the gas-solid phases flow in rotation, the inertia of the solid phase is greater than that of the gas phase, and the relative velocity between the solid and gas phases is greater, which strengthens the mass and heat transfer between the two phases, so the production intensity of the machine is high.
product features
Efficient drying After the wet material enters the bottom of the dryer, it is mechanically crushed under the action of the agitator. The particles with low moisture content and small granularity are entrained and lifted by the rotating airflow, and the drying is completed during the rising process.
Large processing capacity The equipment has simple structure, no wearing parts, and low maintenance costs.
Wide application range In addition, it can also adapt to paste and filter cake-like materials with high moisture content. The moisture content of the material can reach more than 85%, and the final moisture content can be reduced to less than 0.5%.
Energy saving and environmental protection The equipment covers a small area, employs fewer people, and has low comprehensive operating costs.
Intelligent operation The selection of its outlet temperature depends on the final water content requirements of the product, which is usually between 60 and 65 ° C.
Applicable materials
Ceramics: kaolin, silica, clay;
Foods: soy protein, gelatinized starch, distillers grains, wheat sugar, wheat starch, etc.;
Dyes: anthraquinone, black iron oxide, indigo pigment, butyric acid, titanium hydroxide, zinc sulfide, various azo dye intermediates;
Organic matter: atrazine (pesticide), lauric acid, benzoic acid, benzoic acid, germicidal acid, sodium oxalate, cellulose acetate, etc.;
Inorganic: boric acid, calcium carbonate, hydroxide, copper sulfate, iron oxide, barium carbonate, antimony trioxide, various metal hydroxides, various heavy metal salts, synthetic cryolite, etc.
technical specifications
| model | XSG-2 | XSG-4 | XSG-6 | XSG-8 | XSG-10 | XSG-12 | XSG-16 | XSG-20 |
| Inner diameter of main machine mm | 200 | 400 | 600 | 800 | 1000 | 1200 | 1600 | 2000 |
| Air volume M3/h | 350-500 | 1150-2000 | 2450-4500 | 4450-7550 | 7000-12500 | 10000-20000 | 18000-36000 | 28200-56500 |
| Evaporated water kg/h | 12-17 | 40-70 | 80-150 | 150-250 | 230-4250 | 300-600 | 600-1000 | 1000-1500 |
| Maximum installed capacity kw | 10 | 20 | 40 | 65 | 85 | 105 | 150 | 230 |
| Maximum height m | 4.0 | 4.8 | 5.8 | 6.5 | 7.1 | 7.8 | 8.8 | 10.1 |
| Floor area m2 | 15 | 20 | 28 | 35 | 40 | 52 | 80 | 150 |
Note: 1. The moisture evaporation amount is the moisture evaporated per hour when the inlet air temperature is 180 oC and the outlet air temperature is 80oC.
2. In addition to the above models, special designs can be made for users,
3. The above installed capacity is standard, and the power matching can be significantly reduced depending on different materials.
Materials processed and characteristics (based on Type 6 flash evaporation)
| material name | Stearate | Hydroxide-Aluminum | zinc carbonate | monosultap | TMTD | DSD acid | iron oxide red | antimony dioxide | cuprous chloride | White too black |
| Intake air temperature oC | 150 | 180 | 150 | 120 | 140 | 150 | 200 | 180 | 200 | 280 |
| Initial moisture content % | 80 | 55 | 80 | 30 | 65 | 60 | 60 | 45 | 30 | 85 |
| Final moisture content % | 0.5 | 1.5 | 1.0 | 1.0 | 0.5 | 0.5 | 0.5 | 1.0 | 3.0 | 5.0 |
| Actual drying capacity kg/h | 140-160 | 250-280 | 130-170 | 80-110 | 80-120 | 80-120 | 300-350 | 280-320 | 290-310 | 250-300 |
| material name | promoter | oil-soluble ink | manganese zinc substitute | phthalocyanine blue | calcium citrate | superfine calcium carbonate | mud treating agent | sodium dioxyisocyanurate | sodium trioxyisocyanurate |
| Intake air temperature oC | 150 | 150 | 120 | 150 | 140 | 160 | 200 | 180 | 150 |
| Initial moisture content % | 60 | 45 | 30 | 55 | 40 | 70 | 75 | 25 | 30 |
| Final moisture content % | 0.5 | 2.0 | 1.0 | 1.0 | 1.0 | 1.5 | 5.0 | 0.2-2 | 1.0 |
| Actual drying capacity kg/h | 80-110 | 350-380 | 120-150 | 160-180 | 300-350 | 430-470 | 290-310 | 80-120 | 90-150 |
